JPS6242798Y2 - - Google Patents

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Publication number
JPS6242798Y2
JPS6242798Y2 JP1982051645U JP5164582U JPS6242798Y2 JP S6242798 Y2 JPS6242798 Y2 JP S6242798Y2 JP 1982051645 U JP1982051645 U JP 1982051645U JP 5164582 U JP5164582 U JP 5164582U JP S6242798 Y2 JPS6242798 Y2 JP S6242798Y2
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JP
Japan
Prior art keywords
chamber
aeration
pipe
contact aeration
contact
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP1982051645U
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Japanese (ja)
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JPS58156591U (en
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Priority to JP1982051645U priority Critical patent/JPS58156591U/en
Publication of JPS58156591U publication Critical patent/JPS58156591U/en
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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Description

【考案の詳細な説明】 この考案は接触曝気室から沈殿分離室へエアリ
フトポンプによつて常時曝気をうけた汚水等の循
環を行い、沈殿分離室をほぼ好気性とし臭気、ス
カム発生を防止できる分離接触曝気形浄化槽の改
良に関する。
[Detailed description of the device] This device circulates constantly aerated wastewater from the contact aeration chamber to the sedimentation separation chamber using an air lift pump, making the sedimentation separation chamber almost aerobic and preventing the generation of odors and scum. Concerning improvements to separate contact aeration type septic tanks.

従来から、汚水を沈殿分離室で沈殿処理した
後、接触曝気処理する分離接触曝気形浄化槽が提
案されているが、この方式の問題点の1つは剥離
した浮遊汚泥の沈殿分離室への返送である。この
問題点解決するものとして、沈殿分離室と曝気室
との連通口を利用した自然返送、返送用エアリフ
トを利用した間欠返送がある。
Conventionally, separate contact aeration type septic tanks have been proposed in which sewage is subjected to sedimentation treatment in a sedimentation separation chamber and then contact aeration treatment, but one of the problems with this method is that the separated floating sludge is returned to the sedimentation separation chamber. It is. To solve this problem, there are natural return using a communication port between the sedimentation separation chamber and the aeration chamber, and intermittent return using a return air lift.

特にエアリフトを利用した返送方式では確実に
汚泥の返送が行なえるという利点がある反面返送
に長時間を要し、また点検の際に、バルブ切り換
え等の手段でエアリフトポンプを通常一台のフロ
アによつて駆動返送するので、その後の再調整が
難しく、点検時期が少しでも遅れると、SSが放
流されてしまう等の欠点があつた。
In particular, the return method using an air lift has the advantage of being able to return the sludge reliably, but on the other hand, it takes a long time to return the sludge, and during inspections, air lift pumps are usually placed on one floor by means such as switching valves. Since the drive is then sent back, it is difficult to readjust it afterwards, and if there is even a slight delay in inspection, there are drawbacks such as the SS being discharged.

この考案は上記欠点を解消し、沈殿分離室と接
触曝気室の仕切部で水面近くの水中に開口する連
通口と、エアリフトによる沈殿分離室への曝気を
うけた汚水等の循環を常時行うことにより、沈殿
分離室をほぼ好気性とし、臭気、スカム等を防止
し、また、バルブ調整を不用とした分離接触曝気
形浄化槽を提供することを目的とする。
This invention solves the above-mentioned drawbacks, and uses a communication port that opens into the water near the water surface in the partition between the sedimentation separation chamber and the contact aeration chamber, and an air lift to constantly circulate aerated wastewater, etc. to the sedimentation separation chamber. It is an object of the present invention to provide a separation contact aeration type septic tank that makes the sedimentation separation chamber almost aerobic, prevents odor, scum, etc., and does not require valve adjustment.

以下、この考案の一実施例について図面を参照
して説明する。
An embodiment of this invention will be described below with reference to the drawings.

例えばFRP等で形成された槽本体1の内部
は、第1図、第2図に示すように、仕切板2と、
下方連通状のセパレータ3とによつて、沈殿分離
室4と、接触曝気室5と、沈殿室6とに仕切られ
ている。そして、上記槽本体1の一端には、上記
沈殿分離室4内の流入端で、垂直方向に上下端開
放の流入縦管7に接続した流入管8が、他方、他
端には、上記沈殿室6に設けられた消毒室9に連
通して汚水の放流管10がそれぞれ設けられてい
る。
As shown in FIGS. 1 and 2, the inside of the tank body 1 made of FRP or the like includes a partition plate 2,
It is partitioned into a precipitation separation chamber 4, a contact aeration chamber 5, and a precipitation chamber 6 by a separator 3 that communicates downward. At one end of the tank body 1, there is an inflow pipe 8 connected vertically to an inflow vertical pipe 7 with open upper and lower ends at the inflow end in the sedimentation separation chamber 4; A wastewater discharge pipe 10 is provided in communication with a disinfection chamber 9 provided in the chamber 6, respectively.

上記沈殿分離室4の仕切板2側には、剥離され
た汚泥等を接触曝気室5から沈殿分離室4へ戻す
ために、仕切板2に穿設された連通口2aを囲ん
で縦方向に伸びた移流管11が設けられ、沈殿分
離後の汚水を接触曝気室5で導入する。
On the partition plate 2 side of the sedimentation separation chamber 4, in order to return the separated sludge etc. from the contact aeration chamber 5 to the sedimentation separation chamber 4, there are vertically arranged holes surrounding the communication port 2a bored in the partition plate 2. An elongated advection pipe 11 is provided to introduce the wastewater after precipitation separation into the contact aeration chamber 5.

上記接触曝気室5内は上記連通口2a近傍の曝
気撹拌室12と、この曝気撹拌室12の周囲に充
填された接触材13とに仕切られ、この接触
材13の下方には逆洗管14が配置されている。
また、上記曝気撹拌室12には、その下部に配さ
れた散気管15と、曝気をうけた汚水等の循環用
のエアリフト管(エアリフトポンプ)16とが設
けられている。このエアリフト管16の一端は曝
気撹拌室12の下端で開口され、他端は循環水管
16aとして上記沈殿分離室4内の流入縦管7に
連通している。そしてこの循環水管16aのほぼ
水平部分で、かつ沈殿分離室4の点検口1aの真
下位置には、第1図から第3図に示すように、切
り欠きから成る流通状態確認用の監視窓17が設
けられている。
The inside of the contact aeration chamber 5 is partitioned into an aeration stirring chamber 12 near the communication port 2a and a contact material 13 filled around this aeration stirring chamber 12. Below this contact material 13 is a backwash pipe 14. is located.
Further, the aeration stirring chamber 12 is provided with an aeration pipe 15 disposed at a lower portion thereof, and an air lift pipe (air lift pump) 16 for circulating aerated wastewater or the like. One end of this air lift pipe 16 is opened at the lower end of the aeration stirring chamber 12, and the other end communicates with the inflow vertical pipe 7 in the precipitation separation chamber 4 as a circulating water pipe 16a. As shown in FIGS. 1 to 3, in a substantially horizontal portion of the circulating water pipe 16a and directly below the inspection port 1a of the sedimentation separation chamber 4, there is a monitoring window 17 formed of a notch for checking the flow state. is provided.

上記逆洗管14、散気管15およびエアリフト
管16は第4図に示すように、一台のブロアから
の空気管(接続配管)18に接続され、槽本体1
の外部または内部の点検口1a真下等の作業し易
い場所で分岐されている。
As shown in FIG. 4, the backwash pipe 14, air diffuser pipe 15 and air lift pipe 16 are connected to an air pipe (connection pipe) 18 from one blower, and are connected to the tank main body 1.
It is branched off at a place where it is easy to work, such as directly under the inspection opening 1a inside or outside of the.

そして、逆洗管14への空気管18aと、散気
管15、エアリフト管16への空気管18b,1
8cの少なくとも一方とにはバルブ19,20が
設けられ、さらに、逆洗管14は散気管15およ
びエアリフト管16の空気放出端より浅く配置さ
れている。
Then, the air pipe 18a to the backwash pipe 14, the air pipe 18b to the air diffuser pipe 15, and the air lift pipe 16, 1
Valves 19 and 20 are provided on at least one of the air pipes 8c, and the backwash pipe 14 is placed shallower than the air discharge ends of the aeration pipe 15 and the air lift pipe 16.

上記接触曝気室5とセパレータ3で仕切られた
沈殿室6の上部には越流ぜき21を有する消毒室
9が設けられ、この消毒室9には放流管10が連
通されている。
A disinfection chamber 9 having an overflow weir 21 is provided above the contact aeration chamber 5 and the precipitation chamber 6 separated by the separator 3, and a discharge pipe 10 is connected to the disinfection chamber 9.

次にこの考案の作用、効果について説明する。 Next, the function and effect of this invention will be explained.

槽本体1に導入された汚水は沈殿分離、接触曝
気、沈殿、消毒処理を経た後、放流管10から放
流される。平常時には逆洗管14のバルブ19を
閉じ、他方バルブ20によつて散気とエアリフト
との供給空気量の比を調整し、散気管15による
曝気と、エアリフト管16による沈殿分離室4へ
の曝気をうけた汚水等の循環および連通口2aよ
りの剥離汚水の戻りを連続的に行なう。
The wastewater introduced into the tank body 1 is discharged from the discharge pipe 10 after undergoing precipitation separation, contact aeration, precipitation, and disinfection treatment. Under normal conditions, the valve 19 of the backwash pipe 14 is closed, and the other valve 20 is used to adjust the ratio of the amount of air supplied to the diffuser and air lift. Circulation of aerated sewage and return of stripped sewage through the communication port 2a are carried out continuously.

ここで、点検時に逆洗管14のバルブ19を開
くと、逆洗管14の方が散気管15、エアリフト
管16より浅い位置に配置されているため、バル
ブ20を何ら調整することなく、逆洗管14のみ
で曝気が行なわれ、接触材13の逆洗、洗浄が
行なわれる。
Here, when the valve 19 of the backwash pipe 14 is opened during inspection, the backwash pipe 14 is located at a shallower position than the aeration pipe 15 and the air lift pipe 16, so the backwash pipe 14 is opened without any adjustment of the valve 20. Aeration is performed only through the washing pipe 14, and the contact material 13 is backwashed and washed.

その後、逆洗管14のバルブ20を閉じれば、
元の状態通りの曝気および循環が再開される。こ
の際、散気とエアリフトとの比は逆洗時に調整変
更しなかつたので、そのまゝ運転が再開でき、し
かも循環状態は点検口1a下の監視窓17で確認
することができる。
After that, if you close the valve 20 of the backwash pipe 14,
Aeration and circulation resume as before. At this time, since the ratio between air diffusion and air lift was not adjusted during backwashing, operation could be resumed as is, and the circulation status could be confirmed through the monitoring window 17 below the inspection port 1a.

以上のようにエアリフトによる曝気をうけた汚
水等の循環および連通口2aよりの剥離汚泥の戻
りは、常時行われているために、沈殿分離室4内
の大部分を好気性に保持できるので、次の効果を
奏する。
As mentioned above, since the circulation of aerated sewage etc. by the air lift and the return of the peeled sludge through the communication port 2a are always carried out, most of the inside of the sedimentation separation chamber 4 can be kept aerobic. It has the following effects.

沈殿分離室が好気性に保たれるので、室内で
の臭気、スカムの発生を抑えられる。
Since the sedimentation separation chamber is kept aerobic, odor and scum generation inside the room can be suppressed.

沈殿分離室内が希釈され、濃度が低くなつて
いるため、急激な流入があつても、接触ばつ気
室へ高濃度の汚水が流れこむことがなく流入の
シヨツク等が緩和できる。
Since the interior of the sedimentation separation chamber is diluted and the concentration is low, even if there is a sudden inflow, highly concentrated wastewater will not flow into the contact aeration chamber, and the shock of inflow can be alleviated.

沈殿分離室内でも好気性の処理が行なわれ、
全体として汚泥生成量が少なくなる。
Aerobic treatment is also carried out in the sedimentation separation chamber.
Overall, the amount of sludge produced is reduced.

沈殿分離室に沈殿するのは大部分が難分解性
(例えば繊維分)の固形物となる。
Most of what settles in the precipitation separation chamber is hard-to-decompose (eg, fiber) solids.

特に、雑排水等も流入する合併処理浄化槽で
は、ピーク流量の量が非常に大きく、沈殿分離
室の上澄濃度(水質が放流水とほぼ同じ)を低
くしておくと、放流水質が悪化しない。
In particular, in combined treatment septic tanks that also receive gray water, etc., the peak flow rate is very large, and if the supernatant concentration in the sedimentation separation chamber (the water quality is almost the same as the effluent water) is kept low, the quality of the effluent water will not deteriorate. .

第5図は他の実施例を示し、沈殿分離室4を下
方連通状のセパレータ2によつて仕切り、2次沈
殿分離室4aを形成し、エアリフト管16の循環
水管16aをこの2次沈殿分離室4aの上方に配
置した分離接触曝気形浄化槽である。
FIG. 5 shows another embodiment, in which the sedimentation separation chamber 4 is partitioned by a separator 2 communicating with the lower part to form a secondary sedimentation separation chamber 4a, and the circulating water pipe 16a of the air lift pipe 16 is connected to the secondary sedimentation separation chamber 4a. This is a separate contact aeration type septic tank located above the chamber 4a.

この実施例の浄化槽によれば、接触曝気室5内
の曝気をうけた汚水等はエアリフトポンプ作用に
よつて、常時、2次沈殿分離室4aへ循環され
る。このため、2次沈殿分離室4aは好気性に保
たれ、ここでの水質は接触曝気室5内とほぼ同様
になつている。
According to the septic tank of this embodiment, aerated sewage, etc. in the contact aeration chamber 5 is constantly circulated to the secondary precipitation separation chamber 4a by the action of the air lift pump. Therefore, the secondary precipitation separation chamber 4a is kept aerobic, and the water quality here is almost the same as in the contact aeration chamber 5.

一般の浄化槽ではピーク流入の際、水質の悪い
沈殿分離室の上澄液が大量に曝気室へ流入し、負
荷が高くなり水質を悪化させるが、この実施例で
は2次沈殿分離室4aが予備酸化室となり、ピー
ク流入の際、接触曝気室5へ流入する汚水の水質
が良くなり、接触曝気室5に対する負荷が軽減さ
れる。そして、2次沈殿分離室4aの容量は、例
えば、家庭用合併処理であれば風呂ドレーンの容
量とする等ピーク流入量に合わせて設定すると良
い。
In a general septic tank, at the time of peak inflow, a large amount of supernatant liquid from the sedimentation chamber with poor water quality flows into the aeration chamber, increasing the load and deteriorating the water quality, but in this embodiment, the secondary sedimentation chamber 4a is provided as a backup. It becomes an oxidation chamber, and the quality of the wastewater flowing into the contact aeration chamber 5 at the time of peak inflow improves, and the load on the contact aeration chamber 5 is reduced. The capacity of the secondary precipitation separation chamber 4a may be set in accordance with the peak inflow amount, such as the capacity of a bath drain in the case of household combined processing, for example.

第6図に示したものは、さらに他の実施例で、
沈殿分離室内に接触材19,20を充てんした
ものである。
What is shown in FIG. 6 is still another embodiment,
The precipitation separation chamber is filled with contact materials 19 and 20.

沈殿分離室内は仕切板18により、嫌気性室4
bと好気性室4aに区切られる。そして、この仕
切板18に沿つて、エアリフト循環水を下方へ導
く通路4cが設けられている。また、この通路4
cは清掃時のバキユームホースの導入口、および
嫌気性室4bの水位が異常に上昇した際に、その
汚水を好気性室下方に導くオーバーフロー流路も
かねている。嫌気性室4bおよび好気性室4aに
は接触材19,20がそれぞれ充てんされてい
る。
The sedimentation separation chamber is divided into an anaerobic chamber 4 by a partition plate 18.
It is divided into an aerobic chamber 4a and an aerobic chamber 4a. A passage 4c is provided along this partition plate 18 to guide the airlift circulating water downward. Also, this passage 4
C also serves as an inlet for a vacuum hose during cleaning, and an overflow channel that guides wastewater to the lower part of the aerobic chamber when the water level in the anaerobic chamber 4b rises abnormally. The anaerobic chamber 4b and the aerobic chamber 4a are filled with contact materials 19 and 20, respectively.

この実施例では流入汚水はまず嫌気性室4b
で、沈殿分離および嫌気性分解処理を受ける。そ
して、材19を通過したあと連通路4cからの
循環水と混合されて、好気性室4A内の材20
を通過し好気性処理を受ける。好気性処理を受け
た汚水は、接触ばつ気室5に流入し、他の実施例
と同様に処理される。
In this embodiment, the inflowing wastewater first flows into the anaerobic chamber 4b.
It undergoes precipitation separation and anaerobic decomposition treatment. After passing through the material 19, it is mixed with the circulating water from the communication path 4c, and the material 20 in the aerobic chamber 4A is mixed with the circulating water from the communication path 4c.
and undergo aerobic treatment. The wastewater that has undergone aerobic treatment flows into the contact aeration chamber 5 and is treated in the same manner as in the other embodiments.

この実施例では、循環水により好気性室4aが
好気性に保たれるため、接触ばつ気室5に流入す
る水質が非常によく保たれるという効果が得られ
るとともに、材20に付着する好気性微生物に
よる処理も行われるため、非常に効果がよい。さ
らに、嫌気性室4bにおいて材19に保持され
た嫌気性菌により嫌気性分解処理が行われるため
汚泥発生量も少ない。また材が流れに対し抵抗
となるため短絡がなく、流入シヨツクの緩和もは
かれる。
In this embodiment, since the aerobic chamber 4a is kept aerobic by the circulating water, the quality of the water flowing into the contact air chamber 5 is maintained very well. It is very effective because it is also treated with airborne microorganisms. Furthermore, since anaerobic decomposition processing is performed by the anaerobic bacteria held in the material 19 in the anaerobic chamber 4b, the amount of sludge generated is also small. In addition, since the material acts as a resistance to the flow, there is no short circuit, and the inflow shock can be alleviated.

なお、材19,20の一方を省いても、また
第1図に示された区切られていない沈殿分離室に
材を配してもよい。
It should be noted that one of the materials 19 and 20 may be omitted, or the materials may be placed in the undivided sedimentation chamber shown in FIG.

以上のように、この考案の分離接触曝気形浄化
槽によれば、接触曝気室内に循環水用のエアリフ
トポンプを設け、このエアリフトポンプによつ
て、常時沈殿分離室への循環を行つたので沈殿分
離室をほぼ好気性とし、臭気、スカム発生を防止
できる等の効果がある。
As described above, according to the separated contact aeration type septic tank of this invention, an air lift pump for circulating water is installed in the contact aeration chamber, and this air lift pump constantly circulates water to the sedimentation separation chamber, so that sedimentation is separated. It has the effect of making the room almost aerobic and preventing the generation of odors and scum.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図はこの考案の一実施例の縦断面図、第2
図は第1図のA−A線断面図、第3図は返送管の
監視窓部の斜視図、第4図はブロア配管の説明
図、第5図、第6図は他の実施例の縦断面図を示
す。 1……槽本体、4……沈殿分離室、5……接触
曝気室、12……接触撹拌室、13……接触
材、14……逆洗管、15……散気室、16……
エアリフト管(エアリフトポンプ)、18……接
続配管、19,20……バルブ。
Figure 1 is a longitudinal sectional view of one embodiment of this invention;
The figure is a sectional view taken along the line A-A in Figure 1, Figure 3 is a perspective view of the monitoring window of the return pipe, Figure 4 is an explanatory diagram of the blower piping, and Figures 5 and 6 are of other embodiments. A vertical cross-sectional view is shown. 1...tank body, 4...precipitation separation chamber, 5...contact aeration chamber, 12...contact stirring chamber, 13...contact material, 14...backwash pipe, 15...aeration chamber, 16...
Air lift pipe (air lift pump), 18... Connection piping, 19, 20... Valve.

Claims (1)

【実用新案登録請求の範囲】 (1) 槽本体内で仕切形成された沈殿分離室および
接触曝気室と、この接触曝気室内に仕切形成さ
れた曝気攪拌室と、この曝気攪拌室と上記沈殿
分離室の仕切部に設けられ、水面近くの水中で
開口する連通口と、上記曝気攪拌室内に配置さ
れ、汚水の曝気を行う散気管と、上記曝気攪拌
室内に配置され、上記散気管で曝気をうけた汚
水等を上記沈殿分離室へ強制循環させるための
エアリフトポンプとを備えた分離接触曝気形浄
化槽。 (2) 上記エアリフトポンプは、上記接触曝気室内
で曝気をうけた汚水等を上記沈殿分離室へ循環
させる水平の循環水管を有し、この循環水管に
監視窓が設けられていることを特徴とする実用
新案請求の範囲第1項記載の分離接触曝気形浄
化槽。
[Scope of Claim for Utility Model Registration] (1) A precipitation separation chamber and a contact aeration chamber partitioned within the tank body, an aeration stirring chamber partitioned within the contact aeration chamber, and the aeration stirring chamber and the precipitation separation described above. A communication port is provided in the partition of the chamber and opens underwater near the water surface; an aeration pipe is placed in the aeration stirring chamber to aerate the waste water; A separation contact aeration type septic tank equipped with an air lift pump for forcibly circulating received sewage etc. to the sedimentation separation chamber. (2) The air lift pump is characterized in that it has a horizontal circulation water pipe that circulates the sewage, etc. that has been aerated in the contact aeration chamber to the sedimentation separation chamber, and that this circulation water pipe is provided with a monitoring window. A separate contact aeration type septic tank according to claim 1 of the utility model.
JP1982051645U 1982-04-09 1982-04-09 Separate contact aeration type septic tank Granted JPS58156591U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1982051645U JPS58156591U (en) 1982-04-09 1982-04-09 Separate contact aeration type septic tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1982051645U JPS58156591U (en) 1982-04-09 1982-04-09 Separate contact aeration type septic tank

Publications (2)

Publication Number Publication Date
JPS58156591U JPS58156591U (en) 1983-10-19
JPS6242798Y2 true JPS6242798Y2 (en) 1987-11-02

Family

ID=30062353

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1982051645U Granted JPS58156591U (en) 1982-04-09 1982-04-09 Separate contact aeration type septic tank

Country Status (1)

Country Link
JP (1) JPS58156591U (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0742557Y2 (en) * 1990-11-14 1995-10-04 株式会社クボタ Air lift pump for septic tank

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5739695B2 (en) * 1976-12-24 1982-08-23
JPS5745390B2 (en) * 1976-07-21 1982-09-27

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6012633Y2 (en) * 1980-08-12 1985-04-23 積水化学工業株式会社 septic tank
JPS5745390U (en) * 1980-08-30 1982-03-12

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5745390B2 (en) * 1976-07-21 1982-09-27
JPS5739695B2 (en) * 1976-12-24 1982-08-23

Also Published As

Publication number Publication date
JPS58156591U (en) 1983-10-19

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